Processes for preparing alumina and various other products

a technology of alumina and other products, applied in the field of chemistry applied to the production of alumina, can solve the problems of inefficient segregation, inability to remove most of the impurities and especially iron, and inability to achieve adequate removal of iron

Active Publication Date: 2016-07-05
ORBITE ALUMINAE INC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Several of such alkaline processes have the disadvantage of being inefficient to segregate and extract value added secondary products, thus leaving an important environmental impact.
There have also been development work employing hydrochloric acid for the leaching step but, it has been found that such processes were not efficient for removing most part of the impurities and especially iron.
For example, removal of iron was also difficult to be carried out via adequate and economical techniques especially when using continuous processes.

Method used

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  • Processes for preparing alumina and various other products
  • Processes for preparing alumina and various other products
  • Processes for preparing alumina and various other products

Examples

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example 1

Preparation of Alumina and Various Other Products

[0205]As a starting material a sample of clay was obtained from the Grande Vallée area in Québec, Canada.

[0206]These results represent an average of 80 tests carried out from samples of about 900 kg each.

[0207]Crude clay in the freshly mined state after grinding and classification had the following composition:

Al2O3: 15%-26%;

SiO2: 45%-50%;

Fe2O3: 8%-9%;

MgO: 1%-2%;

Rare earth elements and / or rare metals: 0.04%-0.07%;

LOI: 5%-10%.

[0208]This material is thereafter leached in a two-stage procedure at 140-170° C. with 18-32 weight % HCl. The HCl solution was used in a stoichiometric excess of 10-20% based on the stoichiometric quantity required for the removal of the acid leachable constituents of the clay. In the first leaching stage of the semi-continuous operation (step 2), the clay was contacted for 2.5 hours with required amount or certain proportion of the total amount of hydrochloric acid. After removal of the spent acid, the clay was ...

example 2

Preparation of Alumina and Various Other Products

[0222]A similar feed material (bauxite instead of clay) was processed as per in example 1 up to the leaching stage and revealed to be easily leachable under the conditions established in example 1. It provided an extraction percentage of 100% for the iron and over 90-95% for aluminum. The technology was found to be economically viable and no harmful by-products (red mud) were generated. Samples tested had various concentrations of Al2O3 (up to 51%), Fe2O3 (up to 27%) and MgO (up to 1.5%).

example 3

HCl Gas Enrichment and Purification: H2SO4 Route

[0223]H2SO4 can be used for carrying out purification of HCl. It can be carried out by using a packing column with H2SO4 flowing counter currently (see FIG. 4). This allows for converting the recovered HCl into HCl having a concentration above the azeotropic point (20.1% wt) and increase its concentration by about 60 to about 70% at minimum.

[0224]Water is absorbed by H2SO4 and then H2SO4 regeneration is applied where H2SO4 is brought back to a concentration of about 95 to about 98% wt. Water release at this stage free of sulphur is recycled back and used for crystallization dissolution, etc. Packing of the column can comprise polypropylene or polytrimethylene terephthalate (PTT).

[0225]Combustion energy can be performed with off gas preheating air and oxygen enrichment. Oxygen enrichment: +2% represents flame temperature increase by: 400° C. maximum.

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Abstract

There are provided processes for preparing alumina. These processes can comprise leaching an aluminum-containing material with HCl so as to obtain a leachate comprising aluminum ions and a solid, and separating said solid from said leachate; reacting said leachate with HCl so as to obtain a liquid and a precipitate comprising said aluminum ions in the form of AlCl3, and separating said precipitate from said liquid; and heating said precipitate under conditions effective for converting AlCl3 into Al2O3 and optionally recovering gaseous HCl so-produced. These processes can also be used for preparing various other products such as hematite, MgO, silica and oxides of various metals, sulphates and chlorides of various metals, as well as rare earth elements, rare metals and aluminum.

Description

CROSS-REFERENCE TO RELATED APPLICATIONS[0001]The present application is a 35 USC 371 national stage entry of PCT / CA2012 / 000871 filed on Sep. 17, 2012 and which claims priority on U.S. 61 / 535,435 filed on Sep. 16, 2011, on U.S. 61 / 584,937 filed on Jan. 10, 2012, and on U.S. 61 / 668,646 filed on Jul. 6, 2012. These documents are hereby incorporated by reference in their entirety.TECHNICAL FIELD[0002]The present disclosure relates to improvements in the field of chemistry applied to the production of alumina. For example, it relates to processes for the production of alumina via the extraction of aluminum from aluminum-containing materials. These processes can also be efficient for preparing other products such as hematite, MgO, silica and oxides of various metals, sulphates and chlorides of various metals, as well as rare earth elements, rare metals and aluminum.BACKGROUND OF THE DISCLOSURE[0003]There have been several known processes for the production of alumina. Many of them were us...

Claims

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Application Information

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Patent Type & Authority Patents(United States)
IPC IPC(8): C01F7/00C22B21/00C01F7/30C01F7/56C01F5/30C01F7/22C01F17/00C01D3/04C01D5/02C01G49/06C01G49/10C01G49/02C22B59/00C01B33/12C01F5/10C01F17/212C01F17/218C01F17/224C01F17/229C01F17/235
CPCC01F7/56C01F17/0043C01G49/02C01G49/06C01G49/10C22B21/0046C22B21/0053C22B59/00C22B21/0015C01B33/12C01B33/126C01D3/04C01D5/02C01F5/10C01F5/30C01F7/22C01F7/30C01P2006/80Y02P10/234Y02P20/129C01B33/187C01F17/235C01F17/218C01F17/229C01F17/212C01F17/224Y02P10/20C01F5/32C01G23/0475C21B15/006C22B3/10C22B3/44C22B26/22C22B34/1245
Inventor BOUDREAULT, RICHARDFOURNIER, JOELPRIMEAU, DENISLABRECQUE-GILBERT, MARIE-MAXIME
Owner ORBITE ALUMINAE INC
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